Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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LOW PROFILE ELECTROCHEMICAL CELL
BACKGROUND OF INVENTION
[0001] The present disclosure relates generally to electrochemical cells, and
particularly to electrochemical cells having a low profile.
[0002] Electrochemical cells are energy conversion devices, usually classified
as
either electrolysis cells or fuel cells. A proton exchange membrane
electrolysis cell can
function as a hydrogen generator by electrolytically decomposing water to
produce hydrogen
and oxygen gas, and can function as a fuel cell by electrochemically reacting
hydrogen with
oxygen to generate electricity. Referring to Figure 1, which is a partial
section of a typical
anode feed electrolysis cell 100, process water 102 is fed into cell 100 on
the side of an
oxygen electrode (anode) 116 to form oxygen gas 104, electrons, and hydrogen
ions (protons)
106. The reaction is facilitated by the positive terminal of a power source
120 electrically
connected to anode 116 and the negative terminal of power source 120 connected
to a
hydrogen electrode (cathode) 114. The oxygen gas 104 and a portion of the
process water
108 exits cell 100, while protons 106 and water 110 migrate across a proton
exchange
membrane 118 to cathode 114 where hydrogen gas 112 is formed.
[0003] Another typical water electrolysis cell using the same configuration as
is
shown in Figure 1 is a cathode feed cell, wherein process water is fed on the
side of the
hydrogen electrode. A portion of the water migrates from the cathode across
the membrane
to the anode where hydrogen ions and oxygen gas are formed due to the reaction
facilitated by
connection with a power source across the anode and cathode. A portion of the
process water
exits the cell at the cathode side without passing through the membrane.
[0004] A typical fuel cell uses the same general configuration as is shown in
Figure 1.
Hydrogen gas is introduced to the hydrogen electrode (the anode in fuel
cells), while oxygen,
or an oxygen-containing gas such as air, is introduced to the oxygen electrode
(the cathode in
fuel cells). Water can also be introduced with the feed gas. The hydrogen gas
for fuel cell
operation can originate from a pure hydrogen source, hydrocarbon, methanol, or
any other
hydrogen source that supplies hydrogen at a purity suitable for fuel cell
operation (i.e., a
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purity that does not poison the catatlyst or interfere with cell operation).
Hydrogen gas
electrochemically reacts at the anode to produce protons and electrons,
wherein the electrons
flow from the anode through an electrically connected external load, and the
protons migrate
through the membrane to the cathode. At the cathode, the protons and electrons
react with
oxygen to form water, which additionally includes any feed water that is
dragged through the
membrane to the cathode. The electrical potential across the anode and the
cathode can be
exploited to power an external load.
[0005] In other embodiments, one or more electrochemical cells can be used
within a
system to both electrolyze water to produce hydrogen and oxygen, and to
produce electricity
by converting hydrogen and oxygen back into water as needed. Such systems are
commonly
referred to as regenerative fuel cell systems.
[0006] Electrochemical cell systems typically include a number of individual
cells
arranged in a stack, with the working fluids directed through the cells via
input and output
conduits formed within the stack structure. The cells within the stack are
sequentially
arranged, each including a cathode, a proton exchange membrane, and an anode.
The cathode
and anode may be separate layers or may be integrally arranged with the
membrane. Each
cathode/membrane/anode assembly (hereinafter "membrane electrode assembly", or
"MEA")
typically has a first flow field in fluid communication with the cathode and a
second flow
field in fluid communication with the anode. The MEA may furthermore be
supported on
both sides by screen packs or bipolar plates disposed within flow fields.
Screen packs or
bipolar plates may facilitate fluid movement to and from the MEA, membrane
hydration, and
may also provide mechanical support for the MEA.
[0007] In order to maintain intimate contact between cell components under a
variety
of operational conditions and over long time periods, uniform compression is
applied to the
cell components. Pressure pads or other compression means are often employed
to provide
even compressive force from within the electrochemical cell. Pressure pads may
be
fabricated from materials incompatible with system fluids and/or the cell
membrane, thereby
requiring the pressure pad to be disposed within a protective encasing or
otherwise isolated
from the system fluids.
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[0008] While existing internal components are suitable for their intended
purposes,
there still remains a need for improvement, particularly regarding cell
efficiency at lower cost,
weight and size. Accordingly, a need exists for improved internal cell
components of an
electrochemical cell that can operate at sustained high pressures and low
resistivities, while
offering a low profile configuration.
BRIEF DESCRIPTION OF THE INVENTION
[0009] Embodiments of the invention disclose an electrochemical cell having a
membrane electrode assembly (MEA), a first cell separator plate, a second cell
separator
plate, and a carbon layer with integrated flowchannels. The MEA includes a
first electrode, a
second electrode, and a membrane disposed between and in fluid communication
with the
first and second electrodes. The first cell separator plate is disposed on the
first electrode side
of the MEA and defines a first flow field therebetween, the first flow field
being proximate a
first frame member. The second cell separator plate is disposed on the second
electrode side
of the MEA and defines a second flow field therebetween, the second flow field
being
proximate a second frame member. The carbon layer with integrated flowchannels
is
disposed at the first flow field, the flowchannels having a flow width that is
equal to or less
than the width of the webbing between adjacent flowchannels.
[0010] Other embodiments of the invention disclose an electrochemical cell
having an
MEA, a first cell separator plate, a second cell separator plate, and a porous
carbon gas
diffusion layer (GDL). The MEA includes a first electrode, a second electrode,
and a
membrane disposed between and in fluid communication with the first and second
electrodes.
The first cell separator plate is disposed on the first electrode side of the
MEA and defines a
first flow field therebetween, the first flow field being proximate a first
frame member. The
second cell separator plate is disposed on the second electrode side of the
MEA and defines a
second flow field therebetween, the second flow field being proximate a second
frame
member. The GDL is disposed at the first flow field and is in intimate contact
with the MEA.
The GDL has an electrical resistivity of equal to or less than about 0.73 Ohm-
centimeters at a
compressive load at the GDL of about 100 pounds-per-square-inch.
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BRIEF DESCRIPTION OF THE DRAWINGS
[0011 ] Referring now to the figures wherein like elements are numbered alike:
[0012] Figure 1 depicts a schematic diagram of a partial electrochemical cell
showing
an electrochemical reaction for use in accordance with embodiments of the
invention;
[0013] Figure 2 depicts an exploded assembly isometric view of an exemplary
electrochemical cell in accordance with embodiments of the invention;
[0014] Figure 3 depicts an expanded partial section cut through the assembly
of
Figure 2;
[0015] Figures 4-7 depict expanded schematic diagrams of alternative
electrochemical
cells to that depicted in Figure 2;
[0016] Figure 8 depicts a set of curves illustrating a mechanical
characteristic of
different materials suitable for use in embodiments of the invention;
[0017] Figure 9 depicts a set of curves illustrating an electrical
characteristic of
different material arrangements suitable for use in embodiments of the
invention; and
[0018] Figures 10-13 depict alternative configurations of a gas diffusion
layer in
accordance with embodiments of the invention.
DETAILED DESCRIPTION OF THE INVENTION
[0019] Disclosed herein are novel embodiments for an electrochemical cell
having
electrically conductive, elastically compressible, and hydrogen compatible,
carbon
components strategically disposed within the cell.
[0020] Although the disclosure below is described in relation to a proton
exchange
membrane electrochemical cell employing hydrogen, oxygen, and water, other
types of
electrochemical cells and/or electrolytes and/or reactants may be used in
accordance with
embodiments of the invention and the teachings disclosed herein. Upon the
application of
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different reactants and/or different electrolytes, the flows and reactions are
understood to
change accordingly, as is commonly understood in relation to that particular
type of
electrochemical cell.
[0021] Referring to Figure 2, an electrochemical cell (cell) 200 suitable for
operation
as an anode feed electrolysis cell, cathode feed electrolysis cell, fuel cell,
or regenerative fuel
cell is depicted in an exploded assembly isometric view. Thus, while the
discussion below is
directed to an anode feed electrolysis cell, cathode feed electrolysis cells,
fuel cells, and
regenerative fuel cells are also contemplated. Cell 200 is typically one of a
plurality of cells
employed in a cell stack as part of an electrochemical cell system. When cell
200 is used as
an electrolysis cell, power inputs are generally between about 1.48 volts and
about 3.0 volts,
with current densities between about 50 A/ft2 (amperes per square foot) and
about 4,000
A/ft2. When used as a fuel cells power outputs range between about 0.4 volts
and about 1
volt, and between about 0.1 A/ft2 and about 10,000 A/ft2. The number of cells
within the
stack, and the dimensions of the individual cells is scalable to the cell
power output and/or
gas output requirements. Accordingly, application of electrochemical cell 200
may involve a
plurality of cells 200 arranged electrically either in series or parallel
depending on the
application.
[0022] Cells may be operated at a variety of pressures, such as up to or
exceeding
about 100 psi, up to or exceeding about 500 psi, up to or exceeding about 2500
psi, or even
up to or exceeding about 10,000 psi, for example. Cel1200 includes a membrane-
electrode-
assembly (MEA) 205 having a first electrode (e.g., cathode) 210 and a second
electrode (e.g.,
anode) 215 disposed on opposite sides of a proton exchange membrane (membrane)
220, best
seen by now referring to Figure 4. Flow fields 225, 230, which are in fluid
communication
with electrodes 210 and 215, respectively, are defined generally by the
regions proximate to,
and bounded on at least one side by, each electrode 210 and 215 respectively.
A flow field
member 235 may be disposed within flow field 225 between electrode 210, a cell
separator
plate 245 and, optionally, a pressure pad separator plate 250. A pressure pad
255 may be
disposed between pressure pad separator plate 250 and cell separator plate
245. In an
embodiment, cell separator plate 245 is disposed adjacent to pressure pad 255.
In alternative
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embodiments, such as depicted in Figures 5-7 for example, alternative
components may be
used for flow field member 235 and pressure pad 255, as will be discussed
later in more detail
with reference to Figures 5-7. A frame 260 generally surrounds flow field 225
and an
optional gasket 265 may be disposed between frame 260 and pressure pad
separator plate 250
generally for enhancing the seal within the reaction chamber defined on one
side of ce11200
by frame 260, pressure pad separator plate 250 and electrode 210. Another
gasket 270 may
be disposed between pressure pad separator plate 250 and cell separator plate
245 enclosing
pressure pad 255.
[0023] Another flow field member 240 may be disposed in flow field 230. A
frame
275 generally surrounds flow field member 240, a cell separator plate 280 is
disposed
adjacent flow field member 240 opposite oxygen electrode 215, and a gasket 285
is disposed
between frame 275 and cell separator plate 280, generally for enhancing the
seal within the
reaction chamber defined by frame 275, cell separator plate 280, and the
oxygen side of
membrane 220. The cell components, particularly cell separator plates (also
referred to as
manifolds) 245, 280, frames 260, 275, and gaskets 265, 270, and 285 may be
formed with
suitable manifolds or other conduits for fluid flow.
[0024] Membrane 220 comprises electrolytes that are preferably solids or gels
under
the operating conditions of the electrochemical cell. Useful materials include
proton
conducting ionomers and ion exchange resins. Useful proton conducting ionomers
include
complexes comprising an alkali metal salt, alkali earth metal salt, a protonic
acid, or a
protonic acid salt. Useful complex-forming reagents include alkali metal
salts, alkaline metal
earth salts, and protonic acids and protonic acid salts. Counter-ions useful
in the above salts
include halogen ion, perchloric ion, thiocyanate ion, trifluoromethane
sulfonic ion,
borofluoric ion, and the like. Representative examples of such salts include,
but are not '
limited to, lithium fluoride, sodium iodide, lithium iodide, lithium
perchlorate, sodium
thiocyanate, lithium trifluoromethane sulfonate, lithium borofluoride, lithium
hexafluorophosphate, phosphoric acid, sulfuric acid, trifluoromethane sulfonic
acid, and the
like. The alkali metal salt, alkali earth metal salt, protonic acid, or
protonic acid salt is
complexed with one or more polar polymers such as a polyether, polyester, or
polyimide, or
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with a network or cross-linked polymer containing the above polar polymer as a
segment.
Useful polyethers include polyoxyalkylenes, such as polyethylene glycol,
polyethylene glycol
monoether, and polyethylene glycol diether; copolymers of at least one of
these polyethers,
such as poly(oxyethylene-co-oxypropylene) glycol, poly(oxyethylene-co-
oxypropylene)
glycol monoether, and poly(oxyethylene-co-oxypropylene) glycol diether;
condensation
products of ethylenediamine with the above polyoxyalkylenes; and esters, such
as phosphoric
acid esters, aliphatic carboxylic acid esters or aromatic carboxylic acid
esters of the above
polyoxyalkylenes. Copolymers of, e.g., polyethylene glycol with
dialkylsiloxanes, maleic
anhydride, or polyethylene glycol monoethyl ether with methacrylic acid are
known in the art
to exhibit sufficient ionic conductivity to be useful.
[0025] Ion-exchange resins useful as proton conducting materials include
hydrocarbon- and fluorocarbon-type resins. Hydrocarbon-type ion-exchange
resins include
phenolic resins, condensation resins such as phenol-formaldehyde, polystyrene,
styrene-
divinyl benzene copolymers, styrene-butadiene copolymers, styrene-
divinylbenzene-
vinylchloride terpolymers, and the like, that are imbued with cation-exchange
ability by
sulfonation, or are imbued with anion-exchange ability by chloromethylation
followed by
conversion to the corresponding quaternary amine.
[0026] Fluorocarbon-type ion-exchange resins can include hydrates of
tetrafluoroethylene-perfluorosulfonyl ethoxyvinyl ether or tetrafluoroethylene-
hydroxylated
(perfluoro vinyl ether) copolymers. When oxidation and/or acid resistance is
desirable, for
instance, at the cathode of a fuel cell, fluorocarbon-type resins having
sulfonic, carboxylic
and/or phosphoric acid functionality are preferred. Fluorocarbon-type resins
typically exhibit
excellent resistance to oxidation by halogen, strong acids and bases. One
family of
fluorocarbon-type resins having sulfonic acid group functionality is NAFIONTM
resins
(commercially available from E. I. du Pont de Nemours and Company, Wilmington,
DE).
[0027] Electrodes 210 and 215 comprise a catalyst suitable for performing the
needed
electrochemical reaction (i.e., electrolyzing water and producing hydrogen).
Suitable catalyst
include, but are not limited to, materials comprising platinum, palladium,
rhodium, carbon,
gold, tantalum, tungsten, ruthenium, iridium, osmium, alloys of at least one
of the foregoing
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catalysts, and the like. Electrodes 210 and 215 can be formed on membrane 220,
or may be
layered adjacent to, but in contact with, membrane 220.
[0028] In an embodiment, flow field members 235, 240 may be screen packs,
bipolar
plates, or other support members. A screen or bipolar plate capable of
supporting membrane
220, allowing the passage of system fluids, and preferably conducting
electrical current is
desirable. In an embodiment, the screens may comprise layers of perforated
sheets or a
woven mesh formed from metal or strands. These screens are typically comprised
of metals,
such as, for example, niobium, zirconium, tantalum, titanium, carbon steel,
stainless steel,
nickel, cobalt, and alloys comprising at least one of the foregoing metals.
The geometry of
the openings in the screens can range from ovals, circles, and hexagons to
diamonds and other
elongated shapes. Bipolar plates are commonly porous structures comprising
fibrous carbon
or fibrous carbon impregnated with polytetrafluoroethylene or PTFE
(commercially available
under the trade name TEFLON from E. I. du Pont de Nemours and Company).
However,
the bipolar plates are not limited to carbon or PTFE impregnated carbon, they
may also be
made of any of the foregoing materials used for the screens, such as niobium,
zirconium,
tantalum, titanium, carbon steel, stainless steel, nickel, cobalt, and
associated alloys, for
example.
[0029] In a preferred embodiment, and referring now to Figures 2 and 5-7
collectively, flow field member 235 on the hydrogen side of MEA 205 may be a
gas diffusion
layer (GDL) 290 fabricated of carbon and having flowchannels 305 (depicted in
Figures 10-
13), flow field member 240 on the oxygen side of MEA 205 may comprise a porous
pressure
support plate 295, frame 260 and gasket 265 may be integrally combined, and
frame 275 and
gasket 285 may be integrally combined. An alignment pin 300 may be used to
maintain the
alignment of the components of ce11200. Figure 3, which depicts an expanded
partial section
cut through the assembly of Figure 2 through pin 300, exemplifies flowchannels
310 and 315
in frame 260 and 275, respectively.
[0030] Pressure pad 255 provides for uniform compression between cell
components
and may comprise a resilient member or an elastically compressible member.
Where pressure
pad 255 comprises a resilient member, an elastomeric material is preferable.
Suitable
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elastomeric materials include, but are not limited to silicones, such as, for
example,
fluorosilicones; fluoroelastomers, such as KALREZ (commercially available
from E. I. du
Pont de Nemours and Company), VITON (commercially available from E. I. du
Pont de
Nemours and Company), and FLUOREL (commercially available from Minnesota
Mining
and Manufacturing Company, St. Paul, MN); and combinations thereof.
[0031] Where pressure pad 255 comprises an elastically compressible member, a
compressible carbon material absent metal or metallic plating is preferable.
Suitable
compressible carbon materials include, but are not limited to carbon paper,
carbon sheet, or
carbon cloth, such as B-1 carbon cloth or B-2 Toray carbon paper (commercially
available
from E-TEK, De Nora Elettrodi Network) and TGP-H-1.Ot and TGP-H-1.5t
(commercially
available from Toray, Inc.). When used without pressure pad separator plate
250, pressure
pad 255 may be porous to allow passage of water or system gases.
[0032] In an embodiment, it has been found that pressure pad 255 made from
elastically compressible carbon material as herein disclosed, and having an
overall thickness
equal to or greater than about 7 mils (1 mil = 0.001 inches) and equal to or
less than about
125 mils, may produce equal to or greater than about 150 psi (pounds per
square inch) of
contact pressure at MEA 205 at a compression amount of equal to or greater
than about 15%
of its original thickness. Test results relating to various carbon materials
at various
thicknesses showing percent compression of original thickness as a function of
pressure are
illustrated in Figure 8. As illustrated, five materials of elastically
compressible carbon
material (Material A, B, C, D and E) exhibit a contact pressure of equal to or
greater than
about 100 psi at a compression amount of equal to or greater than about 15% of
original
thickness, and a contact pressure of equal to or greater than about 150 psi at
a compression
amount of equal to or greater than about 20% of original thickness. As
depicted, Material A
has an original thickness of 10.8 mil (1 mi1= 0.001 inches), Material B has an
original
thickness of 11.5 mil, Material C has an original thickness of 8.5 mil,
Material D has an
original thickness of 15.3 mil, and Material D has an original thickness of
13.0 mil, thereby
indicating that embodiments of the invention are not limited to any one
material thickness.
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[0033] In an embodiment, it has also been found that pressure pad 255
comprising
elastically compressible carbon material as herein disclosed has an electrical
resistivity of
equal to or less than about 0.73 Ohm-centimeters (Ohm-cm) at a compressive
load of equal to
or greater than about 100 psi, making it suitable for use in the electrical
path of cell 200. Test
results relating to various carbon materials showing electrical resistivity as
a function of
pressure at an electrical current of 125 A (Amps) are illustrated in Figure 9.
As illustrated,
four material arrangements of elastically compressible carbon material
(Material A single
layer, Material A double layer, Material B single layer, and Material C double
layer) exhibit a
resistivity of equal to or less than about 0.73 Ohm-cm at a compressive load
of equal to or
greater than about 100 psi, and even exhibit a resistivity of equal to or less
than about 0.73
Ohm-cm at a compressive load of equal to or greater than about 50 psi. As
depicted, the
material arrangements may have one or more layers, and while only single and
double layers
are depicted, it will be appreciated that the invention is not so limited and
may have any
number of layers that are suitable for the purposes disclosed herein.
[0034] In an embodiment, GDL 290 is fabricated of carbon paper, sheet or cloth
as
herein disclosed, and also includes flowchannels 305, best seen by now refemng
to Figures
10-13. In Figure 10, GDL 290 is depicted having flowchannels 305 pierced
through the
material thickness and contained inboard of the edge of GDL 290. In Figure 11,
GDL 290 is
depicted having flowchannels 305 extending to the edge of GDL 290. In an
embodiment, the
width A of flowchannels 305 is equal to or less than the width B of the
webbing between
adjacent flowchannels 305. In Figure 12, GDL 290 is depicted having
flowchannels 305
embossed within the material thickness and not pierced through the material
thickness. In
Figure 13, GDL 290, similar to that of Figure 10, is depicted having two
layers of material
with their respective flowchannels 305 being oriented 90 degrees to each
other. While Figure
13 depicts only two layers of carbon material for GDL 290, it will be
appreciated that any
number of layers may be employed with their respective flowchannels being
oriented at any
angle suitable for permitting lateral (x, y) and longitudinal (z) flow through
GDL 290. Where
GDL 290 includes flowchannels 305, hydrogen frame 260 may be absent
flowchannels 310.
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[0035] Referring now back to Figures 5-7, various configurations of the
components
within cell 200 are illustrated. In Figure 5, contained within flow field 225
is pressure pad
255 and GDL 290. Here, GDL 290 is a carbon material having integrated
flowchannels 305
(see Figures 10-13), and pressure pad 255 may or may not be a carbon material
(paper, sheet
or cloth). Where pressure pad 255 is compressible carbon, as herein disclosed,
GDL 290 may
be made of a solid carbon material. Where pressure pad 255 and GDL 290 are
both made of
compressible carbon, the respective functions of the two may be combined into
one part, as
depicted in Figure 6, thereby providing for a lower profile cell 200. Where
pressure pad 255
is disposed in intimate contact with electrode 210 of MEA 205, as depicted in
Figure 7,
pressure pad 255 is preferably made of porous carbon that may or may not be
compressible.
Where pressure pad 255 is not compressible, still referring to Figure 7, then
GDL 290 is
preferably compressible, and vice versa.
[0036] As discussed, GDL 290 and pressure pad 255 may either or both be
fabricated
from compressible carbon (paper, sheet or cloth), and as also discussed and
illustrated,
compressible carbon suitable for the purposes disclosed herein preferably
exhibits an
electrical resistivity of equal to or less than about 0.73 Ohm-centimeters at
a compressive
load of equal to or greater than about 100 psi. Also, the compressible carbon
material for the
purposes disclosed herein preferably exhibits a mechanical characteristic
sufficient to
maintain a surface pressure at MEA 205 of equal to or greater than about 150
psi at a
compression amount of equal to or greater than about 15% of its initial
thickness, over an
extended period of time.
[0037] An exemplary embodiment using E-TEK Toray 11.5 mil thick carbon paper
successfully produced equal to or greater than about 150 psi of pressure at
equal to or greater
than about 15% compression of initial thickness, with sustained pressure for
over 2000 hours,
and contemplated sustained pressure for tens of thousands of hours. The
electrical resistivity
of the carbon paper at a pressure greater than about 100 psi was also measured
to be less than
0.73 Ohm-cm.
[0038] In view of the foregoing, some embodiments of the invention may have
some
of the following advantages: a lower profile cell configuration having lower
weight, size and
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cost; fewer plated parts resulting in fewer manufacturing process steps and
process time;
lateral and longitudinal (x, y and z) flow without having to create
microchannels in the cell
frame; and, a hydrogen compatible flow field member that is electrically
conductive,
elastically compressible, and suitable for replacing typical metal-rubber
composite pressure
pads and plated metal screen packs.
[0039] While the invention has been described with reference to an exemplary
embodiment, it will be understood by those skilled in the art that various
changes may be
made and equivalents may be substituted for elements thereof without departing
from the
scope of the invention. In addition, many modifications may be made to adapt a
particular
situation or material to the teachings of the invention without departing from
the essential
scope thereof. Therefore, it is intended that the invention not be limited to
the particular
embodiment disclosed as the best mode or only mode contemplated for canying
out this
invention, but that the invention will include all embodiments falling within
the scope of the
appended claims. Moreover, the use of the terms first, second, etc. do not
denote any order or
importance, but rather the terms first, second, etc. are used to distinguish
one element from
another. Furthermore, the use of the terms a, an, etc. do not denote a
limitation of quantity,
but rather denote the presence of at least one of the referenced item.
